Reducing agent aqueous solution mixing device and exhaust gas post-treatment device

ABSTRACT

A reducing agent aqueous solution mixing device includes an exhaust pipe, an injector, a mixing pipe, an inner pipe and a flow section. The exhaust pipe includes an elbow part and a linear part. The injector is disposed in the elbow part and injects a reducing agent aqueous solution. The mixing pipe receives the reducing agent aqueous solution injected from the injector, and includes an outlet portion formed spaced apart from an inner wall of the exhaust pipe, and a plurality of openings formed on the outer peripheral surface thereof. The inner pipe is disposed in the linear part and allows the exhaust gas to flow through the inside and the outer periphery thereof. The flow section is formed between the outlet portion of the mixing pipe and the inner wall of the exhaust pipe to direct the exhaust gas to the inner pipe.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application claims priority to Japanese Patent Application No.2011-285449 filed on Dec. 27, 2011, the disclosure of which is herebyincorporated herein by reference in its entirety.

TECHNICAL FIELD

The present invention relates to a reducing agent aqueous solutionmixing device, particularly to, a reducing agent aqueous solution mixingdevice for adding a reducing agent aqueous solution to exhaust gas,which is disposed between a filter for trapping particulate substance inthe exhaust gas and a reducing catalyst unit for reducing and purifyingnitrogen oxide in the exhaust gas while being disposed parallel to thefilter. Further, the present invention relates to an exhaust gaspost-treatment device including the aforementioned reducing agentaqueous solution mixing device.

BACKGROUND ART

The exhaust gas of engines contains nitrogen oxide (NOx). An exhaust gaspost-treatment device is disposed at an intermediate position in anexhaust path for inhibiting emission of the nitrogen oxide into the air.The exhaust gas post-treatment device includes a filter for trappingparticulate substance in the exhaust gas, a urea aqueous solution mixingdevice disposed on the exhaust downstream side of the filter in order toadd a urea aqueous solution to the exhaust gas, and a reducing catalystunit disposed on the thither downstream side of the mixing device inorder to reduce and purify nitrogen oxide in the exhaust gas.

The urea aqueous solution mixing device in the aforementioned exhaustgas post-treatment device includes an injector that injects a ureaaqueous solution as a reducing agent into an exhaust pipe. The ureaaqueous solution, injected into the exhaust pipe from the injector, ismixed with the exhaust gas and is supplied to the reducing catalyst uniton the exhaust downstream side. Here, firstly, the urea aqueous solutionis thermally decomposed by the exhaust gas and ammonia is therebyobtained. Then, in the reducing catalyst unit, the ammonia is used as areducing agent and the nitrogen oxide in the exhaust gas is reduced andpurified.

In such device, a sufficient reaction time is required for thermallydecomposing the urea aqueous solution and thereby obtaining ammonia. Toachieve this, it is required to reliably produce a long distance betweenthe injector and the reducing catalyst unit. When the distance is short,the urea aqueous solution injected within the exhaust pipe is notsufficiently mixed with the exhaust gas, while partially attaching asdroplets to the inner wall of the exhaust pipe cooled by the externalair. The urea aqueous solution, thus attached to the inner wall of theexhaust pipe, is not easily decomposed. Therefore, there may bedeficiency in ammonia to be supplied to the reducing catalyst unit.Further, the urea aqueous solution, changed into droplets on the innerwall of the exhaust pipe, may be crystallized and deposited on the innerwall.

In view of the above, as described in Publication of JapaneseTranslation of PCT International Application No. JP-A-2008-509328 andWO2006/025110 A1, devices have been provided that a double-nested pipestructure is produced by disposing an inner pipe within an exhaust pipeon the exhaust downstream side of an injector and a urea aqueoussolution is configured to be injected into the inner pipe. The exhaustgas herein flows around the outer peripheral part of the inner pipe.Therefore, the inner pipe is heated by the exhaust gas, and accordingly,the urea aqueous solution can be inhibited from attaching as droplets tothe inner wall of the inner pipe.

Further, US2010/0263359 A1 and Japan Laid-open Patent ApplicationPublication No. JP-2008-208726 describe devices configured to be capableof sufficiently decomposing a urea aqueous solution even when thedistance from an injector to a reducing catalyst unit is short. In thedevices described in the literatures, a mixing pipe is disposed on thedownstream side of the injector, and urea aqueous solution is configuredto be injected from the injector into the mixing pipe. Further, themixing pipe has a plurality of openings on the outer peripheral surfacethereof. Turbulence is herein generated within the mixing pipe bycausing the exhaust gas to flow into the mixing pipe through theopenings of the mixing pipe. With use of the turbulence of the exhaustgas, dispersion of the urea aqueous solution is promoted and thedecomposition efficiency of the urea aqueous solution into ammonia isenhanced.

SUMMARY

In the devices described in Publication of Japanese Translation of PCTinternational Application No. JP-A-2008-509328 and W02006/025110 A1, theurea aqueous solution injected from the injector is supposed to collideagainst the inner pipe without being sufficiently dispersed, while theparticle size thereof is kept large. Therefore, a large amount of heatis required to evaporate the droplets attached to the inner pipe. Asufficient amount of heat may not be reliably obtained only by theexhaust gas passing around the outer peripheral part of the inner pipe.In view of the above, the devices are required to be provided with aheater and the like as another heat source.

On the other hand, in the devices described in US2010/0263359 A1 andJapan Laid-open Patent Application Publication No. JP-2008-208726, allthe exhaust gas flowing from the upstream side is configured to passthrough the plural openings of the mixing pipe and flow into the mixingpipe, and subsequently, flow downstream. In such configuration, flowpath resistance is increased when the exhaust as passes through themixing pipe, and the back pressure of the engine is increased.Therefore, this results in deterioration in fuel consumption.

It is an object of the present invention to inhibit a reducing agentaqueous solution such as a urea aqueous solution added to exhaust gasfrom attaching to the inner wall of an exhaust pipe, and simultaneously,reduce the flow path resistance within the exhaust pipe, in a devicetier mixing the reducing agent aqueous solution such as a urea aqueoussolution with the exhaust gas.

A reducing agent aqueous solution mixing device according to a firstaspect is a device for adding a reducing agent aqueous solution to anexhaust gas, which is disposed between a filter trapping particulatesubstance in the exhaust gas and a reducing catalyst unit reducing andpurifying nitrogen oxide in the exhaust gas, and includes an exhaustpipe, an injector, a mixing pipe, an inner pipe and a flow section. Theexhaust pipe includes: an elbow part having a curved portion; and alinear part disposed on an exhaust downstream side of the elbow part.The injector is disposed outside the curved portion of the elbow part,and injects the reducing agent aqueous solution into the elbow parttowards the linear part. The mixing pipe has a plurality of openings onan outer peripheral surface thereof and is disposed inside the elbowpart for enclosing a surrounding of the reducing agent aqueous solutionto be injected from the injector and for producing an interval betweenan exhaust downstream side outlet portion thereof and an inner wall ofthe exhaust pipe. The inner pipe is disposed at an internal away from aninner wall of the linear part, and allows the exhaust gas to flowthrough an inside thereof and an outer periphery thereof. The flowsection is formed between the outlet portion of the mixing pipe and theinner wall of the exhaust pipe, and directs the exhaust gas residing inthe outer periphery of the mixing pipe to the inner pipe.

In the device, the exhaust gas, flowing to the elbow part from theupstream side, flows inside the mixing pipe through the openings of theouter peripheral surface of the mixing pipe. Inside the mixing pipe, thereducing agent aqueous solution is injected from the injector.Therefore, the exhaust gas and the reducing agent aqueous solution aremixed inside the mixing pipe. The exhaust gas and the reducing agentaqueous solution, mixed in the fluxing pipe, flow into the downstreaminner pipe. The inner pipe is being heated by the exhaust gas flowingthrough the outer periphery thereof. Even when attached to the innerwall of the inner pipe, the reducing agent aqueous solution isevaporated and changed into ammonia. Therefore, the reducing agentaqueous solution can be inhibited from attaching to the inner wall ofthe exhaust pipe and that of the inner pipe.

Suppose no mixing pipe is herein disposed, the reducing agent aqueoussolution injected from the injector is directed towards the inner wallof the exhaust pipe by means of the impetus of the flow of the exhaustgas flowing thereto from the upstream side, and gets to be easilyattached to the exhaust pipe inner wall.

However, in the present invention, as described above, the reducingagent aqueous solution of the injector is injected inside the mixingpipe, while the exhaust gas flows into the mixing pipe through theopenings of the mixing pipe. Therefore, the injected reducing agentaqueous solution gets to be less affected by the impetus of the exhaustgas, and can be thereby inhibited from attaching to the inner wall ofthe exhaust pipe.

Here, the reducing agent aqueous solution injected from the injector ismixed with the exhaust gas inside the mixing pipe, and the mixedreducing agent aqueous solution and exhaust gas flows through the innerpipe heated by the exhaust gas. Therefore, the reducing agent aqueoussolution is inhibited from attaching to the inner pipe. Accordingly, thedecomposition efficiency of the reducing agent aqueous solution isenhanced.

On the other hand, an interval is reliably produced between the outletportion of the mixing pipe and the inner wall of the exhaust pipe, andserves as the flow section for the exhaust gas. The exhaust gas, flowingfrom the upstream side, is directed to the inner pipe through the flowsection. In other words, the outer periphery of the outlet portion ofthe mixing pipe is opened. Therefore, the flow path resistance in theexhaust pipe is reduced compared to a conventional device configured toinhale all the exhaust gas into the mixing pipe. Therefore, the backpressure of the engine is inhibited and deterioration in fuelconsumption can be prevented.

A reducing agent aqueous solution mixing device according to a secondaspect relates to the device of the first aspect, and wherein the mixingpipe is supported at an end portion thereof disposed oppositely to theoutlet portion by an elbow part wall opposed to the linear part.

In such support structure of the mixing pipe, the vicinity of the outletportion of the mixing pipe is not required to be supported with respectto the exhaust pipe. In other words, it is not required to dispose amember for obstructing the flow of the exhaust gas in the flow sectionbetween the outlet portion of the mixing pipe and the exhaust pipe innerwall. Therefore, the flow path resistance in the exhaust pipe can bereduced.

A reducing agent aqueous solution mixing device according to a thirdaspect relates to the device of the first or second aspect, and whereina predetermined interval is produced between the outlet portion of themixing pipe and an exhaust upstream side inlet portion of the inner pipein a direction arranged along an exhaust stream.

Here, the exhaust gas, flowing through the flow section in the outerperiphery of the mixing pipe, easily gets to flow into the inner pipe.Therefore, the flow path resistance in the exhaust pipe can be furtherreduced.

A reducing agent aqueous solution mixing device according to a fourthaspect relates to the device of the third aspect, and wherein the inletportion of the inner pipe has an inner diameter greater than an innerdiameter of the outlet portion of the mixing pipe.

Here, the exhaust gas and the reducing agent aqueous solution, mixedinside the mixing pipe, smoothly flow into the inner pipe. Further, theexhaust gas, having flown through the flow section in the outerperiphery of the mixing pipe, also easily gets to flow into the innerpipe.

A reducing agent aqueous solution mixing device according to a fifthaspect relates to the device of the fourth aspect, and wherein themixing pipe and the inner pipe are disposed so that an outlet portionopening of the mixing pipe and an inlet portion opening of the innerpipe encompass an injection angular range of the injector.

Here, the outlet portion opening of the mixing pipe is formed wider thanthe diffusion range of the injected reducing agent aqueous solution. Theinjected reducing agent aqueous solution is thereby prevented fromdirectly colliding against the inner wall of the mixing pipe. Therefore,the reducing agent aqueous solution can be inhibited from attaching asdroplets to the inner wall of the mixing pipe. Further, the opening ofthe inlet portion of the inner pipe is wider than the diffusion range ofthe reducing agent aqueous solution. The injected reducing agent aqueoussolution can be thereby efficiently inhaled into the inner pipe.

A reducing agent aqueous solution mixing device according to a sixthaspect relates to the device of any of the first to fifth aspects, andwherein the plural openings of the mixing pipe are formed only in apartial angular range of the mixing pipe in a circumferential direction.

Here, the openings of the mixing pipe are formed only in a part of theouter peripheral surface of the mixing pipe. Therefore, the exhaust gas,inhaled into the mixing pipe through the openings, is supposed to form aconstant stream. Therefore, the flow of the exhaust gas promotes themixture of the exhaust gas and the reducing agent aqueous solution andthe decomposition of the reducing agent aqueous solution.

A reducing agent aqueous solution mixing device according to a seventhaspect relates to the device of the sixth aspect, and wherein the pluralopenings of the mixing pipe are formed either only in first and thirdregions or second and fourth regions where an outer circumference of themixing pipe is equally divided in tour sequentially aligned regions ofthe first region, the second region, the third region and the fourthregion at 90-degree intervals in the circumferential direction.

Here, similarly to the sixth aspect, the exhaust gas inside the mixingpipe forms constant stream. Therefore, the mixture of the exhaust gasand the reducing agent aqueous solution and the decomposition of thereducing agent aqueous solution are promoted.

A reducing agent aqueous solution mixing device according to an eighthaspect relates to the device of any of the first to seventh aspects, andfurther includes a support member including support portions forsupporting a plurality of circumferential portions of an outerperipheral part of the inner pipe with respect to the exhaust pipe at asingle position in a direction arranged along the exhaust stream.Further, except for the support portions, other regions between thesupport member and an outer peripheral surface of the inner pipe allowthe exhaust gas to flow therethrough, and the inner pipe has no openingformed on the outer peripheral surface thereof.

Here, the outer peripheral part of the inner pipe is supported withrespect to the exhaust pipe by the support portions of the supportmember. Further, the exhaust gas smoothly flows through the otherregions except for the support portions in the outer periphery of theinner pipe. Yet further, the inner pipe has no opening formed on theouter peripheral surface thereof. Therefore, a sufficient amount ofexhaust gas is supposed to flow through the outer periphery of the innerpipe. The inner pipe is thereby efficiently heated.

A reducing agent aqueous solution mixing device according to a ninthaspect relates to the device of any of the first to seventh aspects, andfurther includes a support member that supports an exhaust downstreamside outlet portion of the inner pipe with respect to the exhaust pipeand restricts a flow of the exhaust gas residing between the outerperipheral surface of the inner pipe and the inner wall of the exhaustpipe. Further, the outlet portion of the inner pipe has a plurality ofopenings formed on an outer peripheral surface thereof.

Here, the support member restricts the flow of the exhaust gas at theoutlet portion of the inner pipe. Therefore, the exhaust gas in theouter periphery of the inner pipe flows into the inner pipe through theopenings of the outer peripheral surface of the inner pipe in thevicinity of the outlet portion. Therefore, the exhaust gas and thereducing agent aqueous solution are further mixed at the outlet portionof the inner pipe. Therefore, the decomposition of the reducing agentaqueous solution is further promoted.

A reducing agent aqueous solution mixing device according to a tenthaspect relates to the device of any of the first to ninth aspects, andwherein the mixing pipe and the inner pipe are coaxially disposed.

Here, the exhaust gas and the reducing agent aqueous solution, mixed inthe mixing pipe, smoothly flow into the inner pipe.

An exhaust gas post-treatment device according to an eleventh aspectincludes: a filter trapping particulate substance in an exhaust gas; thereducing agent aqueous solution mixing device recited in any of thefirst to tenth aspects disposed parallel to the filter on an exhaustdownstream side of the filter; and a reducing catalyst unit that isdisposed on the exhaust downstream side of the reducing agent aqueoussolution mixing device and reduces and purifies nitrogen oxide in theexhaust gas.

An exhaust gas post-treatment device according to a twelfth aspectrelates to the device of the eleventh aspect, and wherein the reducingcatalyst unit is disposed parallel to the reducing agent aqueoussolution mixing device.

According to the present aspect as described above, the reducing agentaqueous solution added to the exhaust gas can be inhibited fromattaching to the inner wall of the exhaust pipe in the reducing agentaqueous solution mixing device. In addition, the flow path resistancewithin the exhaust pipe can be reduced, and deterioration in fuelconsumption can be inhibited by inhibiting the back pressure of theengine.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a structural diagram of an exhaust gas post-treatment deviceaccording to an exemplary embodiment of the present invention.

FIG. 2 is a cross-sectional structural diagram of a urea aqueoussolution mixing device according to art exemplary embodiment of thepresent invention.

FIG. 3 is a front view of a flange.

FIG. 4 is a diagram illustrating a mixing pipe and an attachmentstructure thereof

FIG. 5 is a right side view of FIG. 4.

FIG. 6 is a diagram for explaining an injection angle of an injector, amixing pipe and an arrangement of an inner pipe.

FIG. 7 is a diagram illustrating the flow of exhaust gas within anexhaust pipe.

FIG. 8 is a diagram illustrating the flow of the exhaust gas within themixing pipe.

FIG. 9 is a diagram, corresponding to FIG. 2, according to anotherexemplary embodiment of the present invention.

FIG. 10 is a diagram illustrating a mixing pipe according to yet anotherexemplary embodiment of the present invention.

DESCRIPTION OF THE EMBODIMENTS Overall Structure

FIG. 1 is a structural diagram of an exhaust gas post-treatment device 1according to an exemplary embodiment of the present invention. Theexhaust gas post-treatment device 1 includes a diesel particulate filter(hereinafter referred to as “DPF”) 1A, a urea aqueous solution mixingdevice 1B and a nitrogen oxide reducing catalyst unit (hereinafterreferred to as “SCR”) 1C, which are sequentially disposed from anexhaust upstream side (hereinafter simply referred to as “an upstreamside”). Each of the devices is disposed in an intermediate portion of anexhaust pipe through which exhaust gas, discharged from a diesel engine(not illustrated in the figure) through an exhaust manifold, flows.

The DPF 1A serves to trap particulate substance in the exhaust gas andis accommodated within a case 4A.

The urea aqueous solution mixing device 1B serves to add a urea aqueoussolution as a reducing agent to the exhaust gas. The added urea aqueoussolution is hydrolyzed and changed into ammonia. The ammonia, togetherwith the exhaust gas, is supplied to the SCR 1C through a connectionpipe 2. It should be noted that the urea aqueous solution mixing device1B will be explained below in detail.

In the SCR 1C, the ammonia from the urea aqueous solution mixing device1B is used as a reducing agent and nitrogen oxide in the exhaust gas isreduced and purified. The SCR 1C is accommodated within a case 4C.

The case 4A accommodating the DPF 1A, the urea aqueous solution mixingdevice 1B, and the case 4C accommodating the SCR 1C are respectivelydisposed parallel to one another. Further, the exhaust downstream side(hereinafter simply referred to as “a downstream side”) end portion ofthe case 4A and the upstream side end portion of the urea aqueoussolution mixing device 1B are coupled, while the downstream side endportion of the urea aqueous solution mixing device 1B and the upstreamside end portion of the case 4C are connected through the curvedconnection pipe 2.

As described above, the case 4A, the urea aqueous solution mixing device1B and the case 4C are disposed in an S-shape, and thereby, an entirelycompact exhaust gas post-treatment device is formed. It should be notedthat an oxidative catalyst unit may be disposed on the upstream side ofthe DPF 1A within the case 4A in order to execute an oxidative treatmentfor unburnt fuel in the exhaust gas. Further, an ammonia reducingcatalyst unit may be disposed on the downstream side of the SCR 1Cwithin the case 4C in order to execute an oxidative treatment forsurplus ammonia.

Urea Aqueous Solution Mixing Device

FIG. 2 illustrates the structure of the urea aqueous solution mixingdevice 1B according to an exemplary embodiment of the present invention.As described above, the urea aqueous solution mixing device 1B isdisposed between the DPF 1A and the SCR 1C. It should be noted that theillustration in FIG. 1 also includes the connection pipe 2 connected tothe downstream side of the urea aqueous solution mixing device 1B.

The urea aqueous solution mixing device 1B includes an exhaust pipe 4B,an injector 5 for injecting a urea aqueous solution, a mixing pipe 6 andan inner pipe 7.

Exhaust Pipe

The exhaust pipe 4B includes an elbow part 10 disposed on the exhaustupstream side (hereinafter simply referred to as “an upstream side”) anda linear part 11 disposed on the downstream side of the elbow part 10.The elbow part 10 and the linear part 11 are both cylindrically formed.

The elbow part 10 is a connection pipe for causing the exhaust gas,flown thereto in an x-direction (a direction that the exhaust gas flowson the upstream side) depicted in FIG. 2, to flow in a y-directionperpendicular to the x-direction. The elbow part 10 has a curved portion10 a. An attachment portion 10 b, formed by a plane arranged along thex-direction, is disposed on the outer part of the curved portion 10 a.In other words, the attachment portion 10 b faces the inlet-portionopening of the linear part 11. Further, a connection flanged portion 10c is formed on the upstream-side end portion of the elbow part 10,whereas a connection flanged portion 10 d is formed on thedownstream-side end portion of the elbow part 10. It should be notedthat apertures into which connection bolts are fitted are formed in theflanged portions 10 c and 10 d.

The linear part 11 is a linear pipe extended along the y-direction. Aconnection-and-support flange (support member) 12 is welded to theupstream-side end portion of the linear part 11, whereas an annularadaptor 13 is welded to the downstream-side end portion of the linearpart 11 in order to connect the connection pipe 2.

As illustrated in FIG. 3, the flange 12 is a rectangular plate member.Apertures 12 a, into which bolts are fitted for connecting the flange 12to the flanged portion 10 d of the elbow part 10, are funned in fourcorner portions of the flange 12. Further, an aperture 12 b, having thesame diameter as the inner diameter of the linear part 11, is formed inthe center part of the flange 12. Yet further, four support protrusions12 c, formed in the same shape, are disposed in the aperture 12 b forprotruding from the outer peripheral side towards the center part. Thefour support protrusions 12 c are disposed at equal angular intervals.

The elbow part 10 and the linear part 11 are coupled by fixing suchflange 12 to the flanged portion 10 d of the elbow part 10 by means ofthe bolts.

Injector

The injector 5 is attached, together with the mixing pipe 6, to theattachment portion 10 b on the outer part of the curved portion 10 a ofthe elbow part 10. The attachment structure will be described below indetail. The injector 5 injects only a urea aqueous solution, withoutmixing it with air, from an injection outlet of the tip thereof into themixing pipe 6 towards the linear part 11. The injector 5, used in thepresent exemplary embodiment, has an injection angle of 25 degrees, andthe center of the injection outlet of the injector 5 is positioned on aline extended from a center axis CL of the liner part 11 of the exhaustpipe 4B.

Mixing Pipe

The mixing pipe 6 is formed as a sub-unit together with a member forfixing the mixing pipe 6 to the elbow part 10 and etc. FIGS. 4 and 5illustrate the sub-unit. It should be noted that FIG. 5 is a right sideview of FIG. 4.

The mixing pipe 6 has a cylindrical shape, and the center axis thereofis coaxial to the center axis CL of the linear part 11. The mixing pipe6 is disposed in a position within the elbow part 10 where the ureaaqueous solution is injected inside from the injector 5. In other words,the mixing pipe 6 is disposed for enclosing the surrounding of the ureaaqueous solution to be injected from the injector 5. The mixing pipe 6has a plurality of openings 6 a formed on the outer peripheral surfacethereof. As illustrated in FIG. 5, the plural openings 6 a are formedonly in a second region B and a fourth region D, where the outercircumference of the mixing pipe 6 is equally divided into foursequentially aligned regions consisting of a first region A, the secondregion B, a third region C and the fourth region D at 90-degreeintervals in the circumferential direction.

A first plate 15 is fixed to an upstream-side end portion (a left-sideend portion in FIGS. 2 and 4), disposed oppositely to the outlet, of themixing pipe 6 by means of welding. As illustrated in FIG. 5, the firstplate 15 has a roughly triangle contour with a curved portion as eachside thereof, and has a pipe fixation portion 15 a, an attachmentportion 15 b and a guide portion 15 c. An end of the mixing pipe 6 isfixed to the pipe fixation portion 15 a by means of welding. Theattachment portion 15 b is formed on the outer peripheral side of thepipe fixation portion 15 a for forming a step with the pipe fixationportion 15 a. The attachment portion 15 b is attached to the attachmentportion 10 b of the elbow part 10 by means of bolts. Further, the guideportion 15 c is formed in the middle part of the pipe fixation portion15 a, while being formed in tapered shape that the diameter thereof isreduced in proportion to distance outwardly away from the pipe fixationportion 15 a. It should be noted that the guide portion 15 c has anopening formed on an end thereof disposed oppositely to the pipefixation portion 15 a.

The first plate 15 has a recessed portion 15 d formed oppositely to themixing pipe 6. A second plate 16 is fixed to the recessed portion 15 dby means of welding while being fitted therein. The second plate 16 isformed in a disc shape and has an aperture 16 a, in which the injectionoutlet of the injector 5 is disposed, in the middle part thereof.Further, the second plate 16 has a plurality of screw apertures 16 h,and the injector 5 is supported by the second plate 16 through the screwapertures 16 b.

Inner Pipe

As illustrated in FIGS. 2 and 3, the inner pipe 7 is formed in acylindrical shape, the outer peripheral surface thereof is supported bythe tips of the support protrusions 12 c of the flange 12, and these arewelded and fixed to each other. Accordingly, the inner pipe 7 isdisposed at an interval away from the inner wall of the linear part 11on the downstream side of the mixing pipe 6. In other words, a doublenested pipe is formed by the inner pipe 7 and the linear part 11.Further, the inner pipe 7 has an inner diameter greater than the outerdiameter of the mixing pipe 6. The inner pipe 7 is disposed at apredetermined distance away from the outlet of the mixing pipe 6.

It should be noted that the inner pipe 7 does not have any opening, slitand etc. formed on the outer peripheral surface thereof. Therefore, theexhaust gas does not flow between the outer periphery and the innerperiphery of the inner pipe 7.

Arrangement of Respective Structural Members

Using FIG. 6, the positional relations among the injector 5 (aninjection angle of the urea aqueous solution), the mixing pipe 6, theinner pipe 7, the exhaust pipe 4B including the elbow part 10 and thelinear part 11 will be explained in detail. As described above, themixing pipe 6 and the inner pipe 7 are herein disposed on the same axis.The injection outlet of the injector 5 is positioned on a line extendedfrom the center axis CL of these members, while being opposed to aninlet-port on opening of the inner pipe 7.

First, an interval exists between the outlet portion (thedownstream-side end portion that corresponds to the right-side endportion in FIG. 6) of the mixing pipe 6 and the inner wall of the elbowpart 10. The mixing pipe 6 is supported only at an end portion thereofdisposed oppositely to the outlet portion thereof by the elbow part 10.Therefore, no member for supporting the mixing pipe 6 is disposed in thespace. In other words, an annular flow section 20 is formed that thereexists no member or the like obstructing the flow of the exhaust gas.Therefore, through the flow section 20, the exhaust gas, flowing theretofrom the upstream side, can flow towards the inner pipe 7 withoutflowing through the inside of the mixing pipe 6.

Further, a predetermined interval L is produced in a y-direction betweenthe outlet portion of the mixing pipe 6 and the inlet portion of theinner pipe 7. In addition, the inlet portion of the inner pipe 7 has aninner diameter di greater than an inner diameter dm of the outletportion of the mixing pipe 6.

With the aforementioned arrangement and dimensional relations, aninjection angular range of the injector 5 (a range inside an angle α (25degrees in the present exemplary embodiment) in FIG. 6) is set to benarrower than the outlet-portion opening of the mixing pipe 6 and theinlet-portion opening of the inner pipe 7. In other words, theoutlet-portion opening of the mixing pipe 6 and the inlet-portionopening of the inner pipe 7 encompass the injection angular range of theinjector 5.

Actions

During the activation of the engine, the exhaust gas is discharged tothe exhaust pipe through the exhaust manifold. The exhaust gas flowstowards the elbow part 10. As depicted with arrows G1 in FIG. 7, theexhaust gas, flowing into the elbow part 10, flows through the openings6 a of the outer peripheral surface of the mixing pipe 6 and flows intothe mixing pipe 6. Further, as depicted with arrows G2 in FIG. 7, theexhaust gas flows through the flow section 20 formed between the outerperipheral surface of the mixing pipe 6 and the inner wall of the elbowpart 10 and is directed to the inner pipe 7.

On the other hand, the urea aqueous solution is injected from theinjector 5 towards the inside of the mixing pipe 6. The urea aqueoussolution is herein injected within a range of 25 degrees about thecenter axis of the mixing pipe 6.

The exhaust gas from the upstream side herein flows towards the regionto which the urea aqueous solution is injected. However, the ureaaqueous solution is injected towards the inside of the mixing pipe 6,whereas the exhaust gas flows into the mixing pipe 6 through theopenings 6 a of the mixing pipe 6. The injected urea aqueous solution isthereby less affected by the exhaust gas. Therefore, the urea aqueoussolution is inhibited from attaching to the inner wall (especially, aregion 10 e in FIG. 7) of the elbow part 10 opposed to the mixing pipe6.

Further, when flowing into the mixing pipe 6 through the openings 6 a ofthe mixing pipe 6, the exhaust gas, flowing through the openings 6 a,firms a helical flow inside the mixing pipe 6 as illustrated in FIG. 8due to the openings 6 formed only in the second region B and the fourthregion D. The helical flow of the exhaust gas is supposed to promote themixture of the exhaust gas and the urea aqueous solution and promotesthe miniaturization of the urea aqueous solution.

As described above, the exhaust gas to which the urea aqueous solutionis added in the mixing pipe 6 and the exhaust gas having flown throughthe flow section 20 flow into the inner pipe 7. The exhaust gas, havingflown through the flow section 20, mainly flows downstream through theouter periphery of the inner pipe 7, i.e., the space between the outerperipheral surface of the inner pipe 7 and the inner wall of the exhaustpipe 4B. The inner pipe 7 is thereby heated. Further, inside the innerpipe 7, the urea aqueous solution is hydrolyzed and changed into ammoniaby means of the heat of the exhaust gas and the water vapor in theexhaust gas.

The urea aqueous solution is herein attached to the inner wall of theinner pipe 7. However, as described above, the inner pipe 7 is beingheated by means of the exhaust gas flowing through the outer peripherythereof. Therefore, chemical reactions are promoted and the urea aqueoussolution is inhibited from attaching to the inner pipe 7.

The ammonia, produced as described above, is supplied together with theexhaust gas to the SCR. Then, the ammonia is used as a reducing agent inthe reducing catalyst unit and nitrogen oxide in the exhaust gas isreduced and purified.

Features

(1) The urea aqueous solution is injected into the mixing pipe 6,whereas the exhaust gas flows into the mixing pipe 6 through theopenings 6 a of the mixing pipe 6. Therefore, the urea aqueous solutionis inhibited from attaching to the inner wall of the elbow part 10.

(2) The openings 6 a are formed only in a partial region of the outerperipheral surface of the mixing pipe 6. Therefore, the exhaust gas,having flown into the mixing pipe 6 through the openings 6 a, becomesthe helical flow. The helical flow of the exhaust gas well disperses theurea aqueous solution injected from the injector 5 and miniaturizationthereof is promoted inside the mixing pipe. Therefore, the exhaust gasand the urea aqueous solution are uniformly mixed.

(3) The exhaust gas, to which the urea aqueous solution is added, flowsthrough the inner pipe 7 heated by the exhaust gas. Therefore, the ureaaqueous solution can be inhibited from attaching and accumulating ontothe inner watt of the inner pipe 7.

(4) The flow section 20 is formed on the outer periphery of the outletportion of the mixing pipe 6. The exhaust gas, having flown from theupstream side, flows into the mixing pipe 6, while flowing through theflow section 20 and being directed to the inner pipe 7. Therefore, theflow path resistance in the exhaust as is reduced within the exhaustpipe 4B and the back pressure of the engine is inhibited.

(5) The mixing pipe 6 is supported only at the end portion thereofdisposed oppositely to the outlet portion thereof by the elbow part 10.No member or the like for Obstructing the flow of the exhaust gas existsin the flow section 20 on the outer periphery of the outlet portion.Therefore, the flow path resistance can be further reduced within theexhaust pipe 4B.

(6) A predetermined interval is produced between the outlet portion ofthe mixing pipe 6 and the inlet portion of the inner pipe 7 in thedirection arranged along the exhaust stream, and the inlet portion ofthe inner pipe 7 has a diameter greater than that of the outlet portionof the mixing pipe 6. Further, the outlet-portion opening of the mixingpipe 6 and the inlet-portion opening of the inner pipe 7 encompass theinjection angular range of the urea aqueous solution to be injected fromthe injector 5. Therefore, the exhaust gas easily flows into the innerpipe 7, and in addition, the urea aqueous solution injected from theinjector 5 is prevented from directly colliding against the inner wallof the mixing pipe 6. Further, the injected urea aqueous solution can beefficiently inhaled into the inner pipe 7.

Other Exemplary Embodiments

The present invention is not limited to the aforementioned exemplaryembodiment, and a variety of changes or modifications can be herein madewithout departing from the scope of the present invention.

(a) FIG. 9 illustrates another exemplary embodiment. In the exemplaryembodiment illustrated in FIG. 9, the inner pipe and the supportstructure thereof, and the connection structure between the elbow partand the linear part of the exhaust pipe are different from those of theaforementioned exemplary embodiment, while the other configurations aresimilar to those of the aforementioned exemplary embodiment.

An exhaust pipe 24 in the present exemplary embodiment is formed by anelbow part 25 and a linear part 26.

The connection portion of the elbow part 25 to the linear part 26 isdifferent from that of the elbow part 10 of the aforementioned exemplaryembodiment, but the other configurations of the elbow part 25 aresimilar to those of the elbow part 10. The linear part 26 has a flangedportion 26 a with a diameter increased upstream on the upstream-side endportion thereof. The elbow part 25 is provided with a flange unit 27,formed by an annular member and a gasket, on the downstream-side endportion thereof. Further, the flanged portion 26 a of the linear part 26is coupled to the flange unit 27 of the elbow part 25. Yet further, thelinear part 26 has four support recessed portions 26 b, recessed to theinner peripheral side, on a roughly intermediate portion thereof in thelongitudinal direction along the exhaust stream.

An inner pipe 30 has a cylindrical shape and makes contact with the foursupport recessed portions 26 b at the outer peripheral surface of theroughly intermediate part thereof in the longitudinal direction.Further, the outer peripheral surface of the outlet-side end portion ofthe inner pipe 30 is supported by the linear part 26 through an annularsupport member 31. The support member 31 is fixed to the outerperipheral surface of the outlet-side end portion of the inner pipe 30by means of spot welding. Therefore, the support member 31 restricts theflow of the exhaust gas flowing through the outer periphery of the innerpipe 30. It should be noted that the term “restrict” herein includes acase of blocking all the exhaust gas flowing through the outer peripheryof the inner pipe 30 and a case of allowing a small amount of theexhaust gas to flow therethrough.

Further, the inner pipe 30 has openings 30 a on the outlet-side endportion thereof across a predetermined upstream-side range except forthe region on which the support member 31 is disposed.

In such exemplary embodiment, the exhaust gas, flowing through the outerperiphery of the inner pipe 30, heats the inner pipe 30 and then theflow thereof is restricted by the support member 31. Further, theexhaust gas, blocked by the support member 31, is directed inside theinner pipe 30 through the openings 30 a of the inner pipe 30. Then, theexhaust gas is again mixed with the urea aqueous solution at the outletportion of the inner pipe 30.

In such exemplary embodiment, the exhaust gas and the urea aqueoussolution can be more efficiently mixed, in addition to advantageouseffects similar to those of the aforementioned exemplary embodiment.

(b) The shape of the mixing pipe and the region in which openings areformed are not limited to those of the aforementioned exemplaryembodiment.

For example, as illustrated in FIG. 10, a mixing pipe 6′ may have such atapered shape with a diameter increased downstream in the injectiondirection. In this case, the urea aqueous solution injected from theinjector 5 can be inhibited from attaching to the inner wall of themixing pipe 6′.

Further in the aforementioned exemplary embodiment, as illustrated inFIG. 5, the openings 6 a are formed in the second region B and thefourth region D of the mixing pipe 6. However, openings may be formed inthe first region A and the third region C, which are opposed to eachother. Further, openings may be formed only in one of the four regions.Each region in which openings are formed is not limited to a 90-degreerange. For example, openings may be formed in a region with an angularrange of either less than 90 degrees or greater than 90 degrees.

(c) In the aforementioned exemplary embodiment, the urea aqueoussolution has been used as a reducing agent. However, the presentinvention can be similarly applied even when another reducing agent isused.

In the reducing agent aqueous solution mixing device according to theillustrated embodiments of the present invention, the reducing agentaqueous solution added to the exhaust gas can be inhibited frontattaching to the inner wall of the exhaust pipe. Further, in thereducing agent aqueous solution mixing device according to theillustrated embodiments of the present invention, the flow pathresistance within the exhaust pipe can be reduced and deterioration infuel consumption can be inhibited by inhibiting the back pressure of theengine.

The invention claimed is:
 1. A reducing agent aqueous solution mixingdevice for adding a reducing agent aqueous solution to an exhaust gas,the reducing agent aqueous solution mixing device being adapted to bedisposed between a filter for trapping particulate substance in theexhaust gas and a reducing catalyst unit for reducing and purifyingnitrogen oxide in the exhaust gas, the reducing agent aqueous solutionmixing device comprising: an exhaust pipe including an elbow part havinga curved portion, and a linear part disposed on an exhaust downstreamside of the elbow part; an injector disposed outside the curved portionof the elbow part, the injector being configured to inject the reducingagent aqueous solution into the elbow part towards the linear part; amixing pipe having a plurality of openings on an outer peripheralsurface thereof, the mixing pipe being disposed inside the elbow part toenclose a surrounding of the reducing agent aqueous solution injectedfrom the injector, an exhaust downstream side outlet portion of themixing pipe being spaced apart from an inner wall of the exhaust pipe;an inner pipe spaced apart from the inner wall of the exhaust pipe inthe linear part, the inner pipe being configured to allow the exhaustgas to flow through an inside thereof and arranged to allow the exhaustgas to flow through a space between an outer periphery of the inner pipeand the inner wall of the exhaust pipe, the inner pipe being a separatemember from the mixing pipe and arranged such that a space existsbetween an exhaust upstream side inlet portion of the inner pipe and theexhaust downstream side outlet portion of the mixing pipe; and a flowsection formed between the outlet portion of the mixing pipe and theinner wall of the exhaust pipe to direct the exhaust gas from an outerperiphery of the mixing pipe to the inside of the inner pipe.
 2. Thereducing agent aqueous solution mixing device recited in claim 1,wherein the mixing pipe is supported at an end portion thereof disposedoppositely to the outlet portion by an elbow part wall facing the linearpart.
 3. The reducing agent aqueous solution mixing device recited inclaim 1, wherein a predetermined interval is formed between the outletportion of the mixing pipe and the inlet portion of the inner pipe in adirection along an exhaust stream.
 4. The reducing agent aqueoussolution mixing device recited in claim 3, wherein the inlet portion ofthe inner pipe has an inner diameter greater than an inner diameter ofthe outlet portion of the mixing pipe.
 5. The reducing agent aqueoussolution mixing device recited in claim 4, wherein the mixing pipe andthe inner pipe are disposed so that an outlet portion opening of themixing pipe and an inlet portion opening of the inner pipe encompass aninjection angular range of the injector.
 6. The reducing agent aqueoussolution mixing device recited in claim 1, wherein the openings of themixing pipe are formed only in a partial angular range of the mixingpipe in a circumferential direction.
 7. The reducing agent aqueoussolution mixing device recited in claim 6, wherein the openings of themixing pipe are formed either only in first and third regions or secondand fourth regions where an outer circumference of the mixing pipe isequally divided in four sequentially aligned regions consisting of thefirst region, the second region, the third region and the fourth regionat 90-degree intervals in the circumferential direction.
 8. The reducingagent aqueous solution mixing device recited in claim 1, furthercomprising: a support member including support portions supporting aplurality of circumferential portions of an outer peripheral part of theinner pipe with respect to the exhaust pipe at a single position in adirection along the exhaust stream so that the exhaust gas flows throughregions between the support member and an outer peripheral surface ofthe inner pipe except for regions where the support portions areprovided, wherein the inner pipe has no opening formed on the outerperipheral surface thereof.
 9. The reducing agent aqueous solutionmixing device recited in claim 1, further comprising: a support membersupporting an exhaust downstream side outlet portion of the inner pipewith respect to the exhaust pipe, the support member being configured torestrict a flow of the exhaust gas in a region between the outerperipheral surface of the inner pipe and the inner wall of the exhaustpipe, wherein the outlet portion of the inner pipe has a plurality ofopenings formed on an outer peripheral surface thereof.
 10. The reducingagent aqueous solution mixing device recited in claim 1, wherein themixing pipe and the inner pipe are coaxially disposed.
 11. An exhaustgas post-treatment device comprising: a filter configured to trapparticulate substance in an exhaust gas; the reducing agent aqueoussolution mixing device recited in claim 1 disposed parallel to thefilter on an exhaust downstream side of the filter; and the reducingcatalyst unit disposed on the exhaust downstream side of the reducingagent aqueous solution mixing device, the reducing catalyst unit beingconfigured to reduce and purify nitrogen oxide in the exhaust gas. 12.The exhaust gas post-treatment device recited in claim 11, wherein thereducing catalyst is disposed parallel to the reducing agent aqueoussolution mixing device.
 13. The exhaust gas post-treatment devicerecited in claim 11, wherein the exhaust pipe of the reducing agentaqueous solution mixing device has a cylindrical shape, with an exhaustupstream side end of the exhaust pipe being connected to the filter andan exhaust downstream side end of the exhaust pipe being connected tothe reducing catalyst unit.
 14. The reducing agent aqueous solutionmixing device recited in claim 1, wherein the linear part of the exhaustpipe, the mixing pipe, and the inner pipe are cylindrical in shape andarranged coaxially with respect to one another.